Measuring and controlling system



June 16, 1942. Lu s 2,286,864

MEASURING AND CONTROLLING SYSTEM Filed Sept. 25, 1940 6 Sheet s-Sheet 1 INVENTOR c/OH/V F. Lay/2s }r ouo/ ATTOR Y -J. F. LUHRS r MEASURING AND CONTROLLING SYSTEM June, 16, 1942.

6 Sheets-Sheet 2 Filed Sept. 25, 1940 fie.

INVENTOR JOHN F LUH/QS June 16, 1942. J. F. LUHRS 2,286,864

MEASURING AND CO NTROLTJING SYS'FEM Filed Sept. 25, 1940 e Sheets-Sheet 3 JOHN F L UHRS H 6 INVENTOR June 16, 1942. J. F. LLJHRS 2,286,864

MEASURING AND CONTROLLING SYSTEM Filed Sept. 23, 1940 6 Sheets-Sheet 4 ZSnventor JOHN F. LUHRS 7 G ttorneg June 16,1942.

.1. F. LUHRS MEASURING AND CONTROLLING SYSTEM Filed Sept 23, 1940 6 Sheets-Sheet 5 JOHN F. LUHRS' (Ittomeg J. F. LUHRS MEASURING AND CONTROLLING SYSTEM June 16, 1942.

6 Sheets-Sheet 6;

Filed Sept. 25, 1940 Zmnentor FIG.

JOHN f? LUHQS (lttorneg Patented June 16, 1942 John F. Luhrs, Cleveland Heights, Ohio, assignor to Bailey Meter Company, a corporation of Delaware Application September 23, 1940, Serial No. 357,848

15 Claims. (Cl. 122-448) This invention relates to the art of measuring and/or controlling the magnitude of a variable quantity, condition, relation, etc., and particularly such a variable condition as the density of a-liquid-vapor mixture, although the variable might be temperature, pressure or any physical, chemical, electrical, hydraulic, thermal or other characteristic.

I have chosen to illustrate and describe as a preferred embodiment .of my invention its adap-r tation to the measuring and controlling of the density and other characteristics of a flowing heated fluid stream, such as the flow of hydrocarbon oil through a cracking still.

Whi1e a partially satisfactorycontrol of the cracking operation may be had from a knowledge of the temperature, pressure and rate of flow of the fluid stream beingtreated, yet a knowledge of the density of the flowing stream at different points in its path is of a considerably greater value to the operator, but was not available prior to the discovery by Robert L. Rude,

as claimed in his copending application Serial No. 152,860 filed July 9, 1937, now Patent No.

2,217,634 dated Oct. 8, 1940.

In the treatment of water below the critical pressure, as in a vapor generatorlia knowledge of temperature, pressure and rate f flow may be sufiicient for proper control, inasmuch as definite tables have been established for interrelation between temperature and pressure and from which tables the density of the liquid or vapor may be determined. However, there are no available tables for mixtures of liquid nd vapor.

In the processing of a fluid, such as petroleum hydrocarbon, a change in density .of the fluid may occur through at least three causes:

'1. The generation or formation of vapor of the liquid, whether or not separation from the liquid occurs.

2. Liberation of dissolved or entrained gases.

3. Molecular rearrangement as by cracking or polymerization.

The result is that no temperature-pressuredensity tables may be established for any liquid, vapor, or liquid-vapor condition of such a fluid, and it is only through actual measurement of the density of a mixture of the liquid and vapor that theoperator may have any reliable knowledge as to the physical condition of the fluid stream at various points in its treatment.

It will be readily apparent to those skilled in the. art that the continuous determination of the density of such a flowing stream is of tremendous importance and value to an operator in controlling the heating, mean density, time of detention in a given portion of the circuit, etc. A continuous knowledge of the density of such a heated flowing stream is particularly advantageous where wide changes in density occur due to formation, generation, and/or liberation of gases, with a resulting formation of liquid-vapor mixtures, velocity changes, and varying-timeof detention in different portions of the fluid path; In fact, for a fixed or given volume of path, a determination of the mean density in that portion provides the only possibility of accurately determining the time that the fluid in that portion of the path is subjected to heating or treatment. By my invention I provide the requisite system and apparatus wherein such information is made available continuously to an operator,

and furthermore may comprise the guiding means for automatic control of the process or treatment.

While illustrating and describing my invention as preferably adapted to the cracking of petroleum hydrocarbon, it is to be understood thatit may be equally adaptable to the vaporization or treatment of other liquids and in other processes.

In the drawings:

Fig. 1 is a diagrammatic representation of density measuring apparatus for a heated fluid stream.

Fig. 2 is similar to Fig. 1 but includes a determination of mean density.

Fig. 3 is a diagrammatic arrangement of the invention in connection with a a heated fluid stream.

7 Figs. 4, 5 and 6 are simplifled'wirlng diagrams of the composite wiring of Fig. 3.

Fig. '7 is a diagrammatic arrangement similar to Fig. 2 but showing certain modifications thereof.

Fig. 8 illustrates in diagrammatic manner a composite of Figs. 2 and 3 including automatic control provisions.

Figs. 9 and 10 are simplified wiring diagrams of the composite wiring of Fig. 11.

Fig. 11 is a diagrammatic arrangement of the invention similar to Fig. 3 but illustrating a further embodiment.

Ref-'"rrlng now in particular to Fig. 1, I indicate a -=onduit I which may be considered as comprising the once through fluid path of an'oil still wherein a portion of the path is heated as by a burner 2. The rate of flow of the charge or relatively untreated hydrocarbon is continuously measured by the rate of flow meter or difierential recorder 3, While a difl'erential recorder 4 is located with reference to the conduit l beyond the heating means or after the flowing fluid has been subjected to heating or other processing.

' temporary increase in the velocity of the flowing fluid. Such an orifice may be inserted in the conduit between flanges as at 5'. The meter 3 is connected by pipes 6, I to opposite sides of the orifice 5 and comprises a liquid sealed U- tube, in one leg of which is a float operatively connected to. position an indicator 8 relative to an index 9. In similar manner the indicator III of the meter 4 is positioned relative to an index I I; the meter 4 being responsive to the differential head across an orifice or similar restriction between the flanges l2.

- The relation between volume flow rate and difi'erential pressure (head) is:

Q=CMV 2g h (1) where v I Q=cu. it. per sec. C=coeflicient of discharge M=meter constant (depends on pipe diameter and diameter of orifice hole) a=acceleration of gravity=32.17 ft. per sec. per

sec. h=difierential headin ft. of the flowing fluid.

The coeflicient of discharge remains substantially constant for any one ratio of orifice diameter to'pipe diameter, regardless of the density a third difierential pressure producing orifice I3A. The heating coil l4 will be hereinafter referred to as a first heating section, while the coil l5 will be referred to as a second heating section. In the preferred arrangement and operation of the still the section I5 is the con- .version or cracking section, and the one in which it is primarily desirable to continuously determine the mean density of the fluid, as well or specific volume of the fluid being measured.

With 0, M and V2 g all remaining constant, then Q varies as the Vh. Thus it will be seen that the float rise of the meters 3, 4 is independent of variation in density or specific volume of the fluid at the two points of measurement and that the reading on the indexes 9, H of differential head is directly indicative of volume flow. If the conduit size and orifice hole size are the same at both meter locations, then the relation of meter readings is indicative of the relation of density and specific volume.

This may readily be seen, for if it were desired to measure the flowing fluid in units of weight, Equation. 1 becomes:

Assuming the same weight rate of flow passing successively through two similaiw spaced orifices 5, l2 and with a change in density as may be caused by the heating means 2, then the density at the second orifice I! may be determined as follows:

as its time of detention or treatment in this section. For that reason I now desirably determine the mean density of the fluid in the section I5 and accomplish this through an interrelation of the differential pressures produced by the same weight flow passing successively through the orifices 5, HA, I3A.

The same total weight of fluid must pass through the three orifices in succession so long as there is no addition to or diversion from the path intermediate the orifices. It is equally apparent that in the heating of a petroleum hydrocarbon, as'bythe coil l4 between the orifices 5 and HA, there will be a change in density of the fluid between the two orifices, and furthermore that an additional heating of the fluid, as by the coil l5, will further vary the density of, the fluid as at the orifice |3A relative to the orifice I2A.

Assume now that the conduit l is of a uniform size throughout and that the orifices 5, HA and I3A are of a uniform opening area and coemcient or characteristic. Through the agency of the meter IS the differential pressure existing across the orifice BA is continuously indicated upon an index l8 by an indicator H. The mean density of the fluid in the conversion section l5 is then obtainedby averaging the density of the fluid at the orifices I2A, I3A. As for example:

The density of the flowing fluid at the orifice I3A may be obtained in the same manner, relative to the density of the fluid at the orifice 5, as was previously determined (3) for the density of the flowing fluid at the orifice I2A. Simplifying this into a single operation, I have:

(1 d 7nd: 12.4;- 13.4

Now as the specific volume increases progressively from locations 5 to IZA to I3A thedifierential pressure across these orifices increases in like manner, and in the operation of such a cracking still it may be that the differential pressure across an orifice ISA will be several times that across the orifice it the orifice sizes are equal. I have therefore indicated at HA, I3A- of Fig. 2 that these orifices may be of an adjustable type wherein the ratio of orifice hole to pipe area maybe varied externally of the conduit max h W-360cfDH/ vol.

where D=diameter of equivalent circular orifice hole in inches c=coefilcient of discharge j=factor of approach sp. vol.==cu. ft./lb.

Now considering that orifice |2A is so adjusted that its cfD is difierent from that of orifice 5, I may then determine the density at |2A as In similar manner I may determine the density at the orifice I3A regardless of the orifice area, so long as I take into'account the c D of the orifice in the above manner. It'will thus be seen that if the specific volume of the flowing fluid increases so rapidly that the 'difierential head at successive orifice locations (for the same design of orifice) becomes many times the value or the difierential head at the initial orifice, it would be impractical to attempt to indicate or record such difierential head relative to a single index or record chart without one or more of the indications or records going beyond the capacity of the index or chart. There are two ready means of overcoming this practical diificulty, the first being an adjustment of the successive orithe indicator 8 from zero to. 100% travel over the index 8, and that for meters 4 and I8 it requires 250" water difierential to cause the indicator It to move from zero to 100% over the index II, and I1 relative to Hi. Then:

F3=% float travel of meter 3 F4=% float travel of meter 4 In Fig. 3 I show in diagrammatic fashion an arrangement similar to that of Fig. 2, but adapted to give further indications valuable as a guide to operation of the system by manual or automatic means. Herein I illustrate mechanism under the control of the meters 3, 4, It for making. directly and visually available the information I desire for the manual or automatic control of the cracking still.

In the operation of such a cracking still it is of considerable importance to determine, in addition to the mean density, the time of detention of the fluid in various portions of the fluid flow path. It is also of importance to determine the time-temperature relation of the conversion section. For example; the time that any particle remains in this section and the temperature to which it is subjected, or the temperature at which the mixture leaves the section. To determine such temperature I indicate in Fig. 2 at IS the bulb of a gas-filled thermometer system of which 28 indicates the connecting capillary and 2| a Bourdon tube whose free end-is positioned responsive to the temperature at the bulb location.

According to Equation 5 it is necessary, in determining the mean density of the conversion section, to obtain the ratio of the differential heads at orifices 5 and HA. Then to obtain the ratio of the differential heads at orifices 5 and fices, such as HA, HA to have new values of cfD such that the indicator or recording pen will be kept on the chart; and the second through varying the basic capacity 01 the meter t or 16 relative to the meter 3. This latter method is accomplished by so arranging the meter 4, for example, that it requires 50% greater difierential pressure to move the related pointer over full index range than in the case 01 meter 3. This may readily be accomplished by properly proportioning the two legs of the mercury U-tube, on one of which the fioat is carried. 01 course it will be necessary to take such changes in capacity into account when utilizing-the differential head readings in determining density or mean density. V

For example the reading of the pointer relative to the index should be on a percentage basis of whatever maximum head .the meter is designed for. Then the total head corresponding to the indicator reading will be available or the proper correction may be applied. Assume that position a contact arm relative to a resistance forming an arm of a Wheatsone bridge. The system lends itself readily to the remote grouping of the apparatus necessary to indicate the individual values or relations and which Idesirably locate convenient to the operator for hand or automatic control of the process.

The arm 8 of.meter 3 is of insulating material but carries a conducting portion adapted to continuously contact a metallic segment 22 and to movably engage a rhecstat 23 providing a resistance RC representative of the position of the float oi meter 3, or F3. A second conducting portion on the arm 8 contacts a metallic segment 24 and movably engages a rhecstat 25 providing a resistance RCI. In similar manner the arm l0 provides a resistance RI representative of F4; and the arm l'l provides a resistance R0 representative of Fm.

Referring now to Fig. 4 it will be observed that the adjustable resistances RC and RI comprise two arms of a Wheatstone bridge. A third arm includes a hand adjustable resistance F, while a fourth arm includes'a fixed resistance FI andan adjustable resistanceBi. The value of the resistance Fl is substantially the same as of the resistance F. The resistance BI is known as the balancing. resistance and is varied by movement of the arm 30 through the agency of the reversible synchronous motor 31 under control of a galvanometer 32.

The motor 3| is of the self-starting synchronous type of alternating current motor and is shown as having normally energized opposed fields. Should the Wheatstone bridge become unbalanced, then the needle of the galvanometer 32 will move either clockwise or counterclockwise (Fig. 3), thereby open circuiting one of the fields of the motor 3|, resulting in a positioning of the arm 30in direction and amount over the resistance BI to balance the bridge and .cause the galvanometer needle to return to neutral position. It will be understood that the necesh lZA X H5;

Now

Rc hs Rl hm Ro hisa and it is expected that:

It is known that the law of theWheatstone bridge is:

RI B1+F1 When RC and RI are both zero; then the p value of Bi is zero; F equalling Fl.

When RI RC then the index 33 may be ar ranged to read the density dun directly. The resistance Bl will tend to vary from 0 to However, as the value of resistance BI! is to be directly representative of dlflA .the rheostat Bl I must be shaped as the reciprocal of RI/RC or as RC/RI, and will tend to vary as the reciprocal of 0 to In like manner the value of dm may be indicated on the index 34 and be continuously represented by the value of the resistance 32!.

As clearly indicated the same power source 36 is alternatively used for both .bridges. A motor 31 for the second bridge is under the control of a galvanometr 38 connected across the points 21, 35.

In the second bridge a hand adjustable resistance'FF has substantially the same resistance value as'"F2. "In tact-under zero flow conditions the values of F, FI, FF, and F2 should be equal.

A time motor driven cam I00 continuously reciprocates a switch i0! alternatively connecting the power source36 into the two bridges. When either bridge is not connected to the power source 36 the galvanometer of that bridge remains at its neutral position and the various resistance values remain unchanged until the power source 36 is again connected to that bridge.

It will now be observed that the resistance B is representative of the value dim while the resistance B2l is representative of the value (113A. To determine the mean density of the fluid through the conversion sectionli (1714115) I obtain the average of the ratios of heads (Equation 5) and accomplish this by including the resistances Bl I and 132i in'a third bridge circuit (Fig. 5). In this bridge circuit the value of the fixed resistance A is twice that of the value of the fixed resistance B. The adjustable resistance B3 is varied by the positioning of an arm 39, through the agency of a motor 40, under the control 'of a galvanometer 4|.

but

and

for taking care of variations in density of the,

fluid at the orifice 5 which may occur from time to time.

In similar fashion I design into the apparatus the expected value of cfD in connection with the resistance RI and also for the expected value of cfD in conection with the resistance R0. The auxiliary resistance F is moved by hand when a change in the cjD? value for the orifice HA is made by the adjustable means provided. In the same manner, ifthe adjustable orifice HA is moved to anew position and value of cfD the resistance FF is correspondingly varied. The

resistances F, FF may be provided with indexes v graduated to read in cfD values for the corresponding orifice, or in fact they may be so connected as to be moved simultaneously by and with the means provided for moving the adjustable orifices. Reference to Fig. 7 will show that the stem of the adjustable orifice IZA is provided with an indicator I02 movable relative to an index I03 which may be graduated in cfD values; and that the. stem also carries a contact movable along the resistance F. In like manner the arrangement in connection with the adjustable orifice I3A is shown in Fig. 7. Thus at any time the position of an orifice 12A or I3A is varied, the necessary corresponding variation in the resistance value F or FF may be simultaneously accomplished.

The arm 8 is adapted to vary a resistance RCI proportional to I15 which so long as d5 remains constant equals W, where W is rate of flow in pounds per unit of time. This value is then included as an arm in a Wheatstone bridge cir- Tx=time any particle is in section 15.

V=volume between IZAand |3A (cu. ft.)

md15=mean density (lbs. per cu. ft.) W=rate of flow (lbs. per unit T) The resistance T is varied through movement of an arm positioned by amotor 52, under the control of a galvanometer 53. An index 54 may be graduated to read directly in value of time of detention of any particle in the section l5. In order that the resistance RCI will represent the value of W or rate of flow in pounds perunit of time the resistance 25 is shaped according to the Vhs. a

With the resistance T, is varied a resistance Tl, representative of time of detention, and this is incorporated in a bridge circuit (Fig. 6) in relation to a resistance TE, representative of value of temperature, positioned by the Bourdon tube 2|. The bridge circuit of Fig. 6 includes a resistance TT varied by an arm 59 moved by a motor filL'under the control of a galvanometer 6! for advising desired ratio or relation between time and temperature represented respectively by TI and TE. This relationship may be continuously recorded as at 62. Hand adjustable rheostats 63, 64 allow adjustment for constants of time and temperature as may become necessary.

In Fig. '7, previously referred to, the valve H14 in the fuel supply line 2 controls the heating,

while the valve I05 in the conduit l controls the weight rate of flow of fluid to be treated either or both of these values may be manipulated by hand from indications of density, mean density, time of detention, time-temperature relation, or in fact from any of the indications previously referred to in connection with Figs. 1-7, in-

clusive. W

In Fig. 8, I illustrate a composite of Figs. 2 and 3 in which the arms 3|], 30', 5|, 39, or 59, each position an air pilot valve of the general type disclosed and claimed in the Johnson Patent No. 2,054,464 to establish an air loading pressure representative of density, mean density, etc. In Fig. 8 the fuel control valve I06 and the flow control valve 10! are spring loaded diaphragmactuated valves responsive to any or all of the air loading pressures established by the pilot valves, through hand selecting valves I98 or I99, thus I may automatically control the flow and/or heating responsive to determined density or any of the variables mentioned.

In Fig. 11 I illustrate a further arrangement to obtain a manifestation of time of detention or treatment. The charge meter 3 positions the arm 8 relative to a shaped 'or graduated resistance 25 to provide an impedance representative of V755 or W, i. e. the shape of the resistance winding corrects for the quadratic relation between difierential head k5 across the orifice 5 and weight rate of now W. The value of the impedance or electrical resistance 25 in one leg of the Wheatstone bridge of Fig. 9 is then proportional to W the weight rate of fluid flow through the treating system.

In Figs, 9and 11 the impedance values of RI and R0 are respectively representative of hm and him. The bridges of Fig. 9 alternately solve for values N and M in manner similar to that described in connection with Fig. 3. Moved with N is an impedance NI representative of W/hma and moved with M is an impedance Ml repre- .sentative of W/hm.

The two are algebraically added through the bridge of Fig. 10 to determine time of .detention or treatment T, from:

K h 13.4 r X 5 134 its and V volume (a constant) W KEV h5d5 im and im are taken care of by F, FF, X and Y.

It will therefore be seen that through the arrangement of Figs. 9, l0 and 11 it is not necessary to first solve for dlZA and (113A. (as in Fig. 3) to obtain a manifestation of time. Obviously, the time value or position of Fig. 8 may be either that of Fig, 3 or that of Fig. 11.

While I have chosen to illustrate and describe the functioning of my invention in connection with the heating of petroleum or hydrocarbon oil, it is to be understood that the method and apparatus is equally applicable to the treatment, processing, or working of other fluids, such for example, as in the vaporization of water to form 1 steam.

This application constitutes a continuation-inpart of my application Serial No. 152,857 filed July 9, 1937, now Patent No. 2,217,639 dated Oct. 8, 1940.

What I claim as new, and desire to secure by Letters Patent of the United States, is:

1. In a fluid heater having a fluid path, means for exhibiting the relationship between the temperature at a point in the fluid path and the passage. time of: the fluid between two points in the path, comprising in combination, means in said fluid path at the entrance to the heater,

and at each of the points to measure the velocity or flow, impedances varied by each of said last named means, a first Wheatstone bridge including an impedance responsive to velocity of flow at the entrance to said heater, an impedance responsive to velocity of flow at one of the points, and abalancing impedance; a second Wheatstone bridge including an impedance responsive to velocity of flow at the entrance to said heater, an impedance responsive to velocity of flow at the other of said points, and a balancing impedance; automatic means for varying said balancingimpedances to maintain said bridges in balance, a third Wheatstone bridge including impedances proportional to said two balancing impedances in one leg and a balancing impedance in another leg, a fourth 'Wheatstone bridge including an impedance proportional to the last named balancing varied -by the said means measuring the velocity of flow at the entrance to the heater, and a balancing impedance, automatic means for varying said balancing impedance to maintain said fourth Wheatstone's bridge in balance, a fifth Wheatstone bridge including an impedance proportional to the last named variable impedance and an impedance varied in accordance with the temperature of the fluid at a pointin said path, and a balancing impedance; automatic means for varying said balancing impedance to maintain the fifth Wheatstone bridge in balance; and an indicating element positioned by said last named means.

2. In a fluid treating system having a once through fluid path wherein the weight rate of flow at all points in the path is the same and means for heating a section of said path, means for determining the time of treatment of the fluid comprising in'combination, means for obtaining an electrical eflect representative of weight rate 'of fluid flow, means for obtaining an electrical effect representative of the mean fluid density through the treating zone, and electrical means for solving the equation where T is time of detention, V is the volume of the treating zone, md is the mean density of the fluid and W is the weight rate of flow. I

3. In a fluid treating system having a once through fluid path wherein the weight rate of flo'w at all points in the path is the same and means for heating a section of said path, means for determining the time of treatment of the fluid comprising in combination, means for obtaining an electrical effect representative of weight rate of fluid flow, means for obtaining an electrical efl'ect representative of difl'erential pressure hr across an orifice at the inlet to the treating zone, means for obtaining an electrical effect representative of differential pressure he across an orifice at the outlet of the treating zone, and electrical means for solving the equation V W W where Tis time of detention, V is the volume of the treating zone, and W is the weight rate of flow.

4. The method of controlling the operation of a fluid heater having a once through flow path, which includes, establishing electrical impedance values each representativeof a variable condition of the. flowing fluid, continuously interrelating such values and thereby determining an electrical impedance value representative of-the time of detention of the fluid in the heater, utilizing such determined value in ascertaining the time of detention of the fluid in the heater, establishing an optimum time of detention for the fluid in' the heater, and so controlling the heating by use of the ascertained actual time of detention as to maintain the desired optimum time of detention.

5. The method of operating a fluid treating system having a once through fluid flow path, which includes, establishingelectrical impedance values each representative of a variable condition impedance, an impedance of the flowing fluid, continuously interrelating such values and thereby establishing an electrical impedance value representative of the time of detention of the fluid in the path while being treated, utilizing such value in ascertaining the time of detention of the fluid in the treating zone, establishing an optimum time of detention for the fluid in the treating zone, and 'so controlling the rate of fluid flow through the path by use of'the ascertained actual time of detention as to maintain the desired optimum time of detention.

6. The method of controlling the operation of a fluid heater having a once through fluid flow path, which includes, establishing electrical impedance values each representative of a variable condition of the flowing fluid, continuously interrelating such values and thereby determining an electrical impedance value representative of the time of detention of the fluid being heated, utilizing such determined value in ascertaining the time of detention of the fluid in the heater, establishing an optimum time of detention for the fluid in the heater, and so controlling both the heating and the rate of fluid flow through the path by use of the ascertained actual time of detention as to maintain the desired optimum time oi. detention.

7. The method of operating a fluid treating system having a once through fluid flow path, which includes, establishing electrical impedance values each representative of a variable condition of the flowing fluid, continuously interrelating such values and thereby establishing an electrical impedance value representative of the time of treatment of the fluid, treating the flowing fluid by varying its heat content, utilizing such determined value in ascertaining the time of detention of the fluid in the treating zone, establishing an optimum .time of detention 'for the fluid in the treating zone such as to result in desired heat content in the leaving fluid, and so controlling the heat content of the fluid by use of the ascertained actual time of detention as to maintain the desired optimum time of detention and consequently the desired optimum heat content of the fluid leaving the treating system.

8. In a fluid heating system having a forced circulation fluid flow path wherein the weight rate of flow at all points in the path is the same and means for heating a section of said path, means for determining the time of treatment of the fluid comprising in combination, means continuously establishing an electrical impedance value representative of weight rate of fluidflow, means continuously establishing an electrical impedance T: Vmd

where T is time of detention, V is the volume of the treating zone, md is the mean density of the fluid and W is the weight rate of flow.

.the fluid comprising in combination, means continuously establishing an electrical impedance value representative of weight rate of fluid -flow,

means continuously establishing an electrical impedance -value representative of difierential pressure hr across an orifice at-the inletto.the treating zone, means continuously establishing an electrical impedance value representative of differential pressure ho across an orifice at the outi let of the treating zone, and a Wheatstone bridge circuit continuously solving the equation V W W a n 1.

where T is time of detention, V is the volume of the treating zone and W is the weight rate of flow.

10. Apparatus for controlling the operation of a fluid treating system having a iorced'circulation fluid flow path comprising in combination, means continuously establishing an electrical impedance value representative of .the time of detention of the fluid in the treating zone, means for heating the fluid as it flows through the treating zone to maintain the condition of the fluid at optimum, and control means continuously positioning the heating means responsive to the first named means.

11. Apparatus for controlling the operation of a fluid treating system having a forced circulation fluid flow path comprising in combination, means continuously establishing an electrical impedance value representative of the time of detention of the fluid in the treating zone, means for heating the fluid as it flows through the treating zone to maintain the condition of the fluid at optimum, and control means continuously regulating the weight rate of fluid flow through the treating zone responsive to the first named means.

12. The method of controlling the operation of a fluid heater having a once through flow path, which includes, establishing electrical impedance values each representative of a variable condition of the flowing fluid, continuously interrelating such values and thereby establishing an electrical impedance value representative of the time of detention of the fluid in the heater,

establishing an optimum time of detention for the fluid in the heater, and so controlling the heating by use of the established actual electricalimpedance value as to maintain the desired optimum time of detention.

13. The method of operating a fluid treating system having a once through fluid flow path, which'includes, establishing electrical impedance values-each representative of a variable condition of- -the flowing fluid, continuously interrelating such values and thereby establishing an electrical impedance value representative of the time of detention of the fluid in the path while being treated, establishing an optimum time of detention for the fluid in the treating zone, and so controlling the rate of fluid flow through the path by use of the established actual electrical impedance value as to maintain the desired optimum time of detention.

14. The method of controlling the operation of a fluid heater having a once through fluid flow path, which includes, establishing electrical impedance values each representative of a variable condition of the flowing fluid, continuously interrelating such values and thereby establishing an heating and the rate of fluid flow through the path by use of the established actual electrical impedance value as to maintain the desired optimum time of detention.

15. The method ofoperating a fluid treating system having a once through fluid flow path, which includes, establishing electrical impedance values each representative of a variable condition of the flowing fluid, continuously interrelating such values and thereby establishing an electrical impedance value representative of the time of treatment of the fluid, establishing an optimum time of detention for the fluid in the treating zone such as to result in desired heat content in the leaving fluid, and so controlling the heat content of the fluid by use of the established actual electrical impedance value as to maintain the desired optimum time of detention and consequently the desired optimum heat content of the fluid leaving the treating system.

JOHN F. LUHRS.

Certificate of Correction Patent No. 2,286,864. June-16,1942.

JOHN F. LUHRS It is hereby certified that errors appear in the printed specification of the abovenumbered patent requiring correction as follows: Page 2, secondcolumn, lines 61 It it read page 5, first column, lines 51 and 52, for treated either or. both of these values read treated. Either or both of these valves; and that the said Letters Patent should be read with these corrections therein that the same may conform to the record of the case in the Patent Oflice.

Signed and sealed this 8th day of September, A. D. 1942.

HENRY VAN ABSDALE Acting Commissioner of Patents. 

